[0001] The present invention relates to an aluminum nitride powder and a thermally conductive
grease composition using such a powder. Specifically, the invention concerns an aluminum
nitride powder which has improved water resistance and can function effectively as
a heat reducing material when filled into grease or the like, and further to a thermally
conductive grease composition which utilizes the aforesaid aluminum nitride powder
to ensure high water resistance therein and acquire thermal conductivity adequate
for the heat reduction of electronic devices.
[0002] Most electronic devices generate heat while they are used, so that the removal of
the generated heat therefrom is necessary for their normal operation. For the reduction
of the heat from electronic devices, it has been expected to make good use of aluminum
nitride having high thermal conductivity and excellent electric insulating properties.
In applying it to electronic devices, the aluminum nitride can be used in various
forms, including moldings and fillers for grease and synthetic rubber.
[0003] However, aluminum nitride is inferior in water resistance, particularly in a pulverized
state. More specifically, the aluminum nitride in pulverized state is gradually decomposed
while it is allowed to stand in the air, thereby evolving ammonia to be converted
into aluminum hydroxide. Therefore, the problem confronting the use of an aluminum
nitride powder, e.g., as a filler for heat reduction of resins is poor water resistance
of the powder.
[0004] Some attempts have been made at improving the water resistance of an aluminum nitride
powder. For instance, the improvement of water resistance has been attempted by coating
the surface of an aluminum nitride powder with an organic high molecular compound,
or by oxidizing the aluminum nitride powder surface to form a protective film of aluminum
oxide. Further, Japanese Tokkai Hei 4-321506 (the term "Tokkai" as used herein means
an "unexamined published patent application") proposes the art of forming a coating
on the aluminum nitride powder surface through the reaction between an organosilane
oligomer and an silanol group-containing polyorganosiloxane in the presence of a catalyst.
[0005] However, none of those methods are successful in conferring sufficient water resistance
upon aluminum nitride. Thus, the application of such aluminum nitride powders to a
silicone grease composition for heat reduction use has a defect that the resulting
composition suffers gradual deterioration in heat reduction characteristics.
[0006] As a result of our intensive studies to improve the water resistance of an aluminum
nitride powder, it has been found that an aluminum nitride powder having high water
resistance can be obtained by the surface treatment of aluminum nitride with a specified
organosilane and/or partial hydrolysis condensate thereof, thereby achieving the present
invention.
[0007] Therefore, a first object of the present invention is to provide an aluminum nitride
powder which has high water resistance and is effectively used as a filler to constitute
a heat reducing material.
[0008] A second object of the present invention is to provide a grease composition for heat
reduction use which shows high resistance to water although an aluminum nitride powder
is used therein as a filler.
[0009] According to a first aspect of the present invention there is provided an aluminum
nitride powder having the surface treated with an organosilane represented by formula,
R
IaR
IIbSiY
4-1-b, and/or a partial hydrolysis condensate thereof, wherein R
I represents a 6-20C alkyl group or a group formed by substituting halogen atom or
atoms for part or all of the hydrogen atoms attached to carbon atoms of the 6-20C
alkyl group, R
II represents a 1-20C hydrocarbon group or a group formed by substituting halogen atom
or atoms for part or all of the hydrogen atoms attached to carbon atoms of the 1-20C
hydrocarbon group, Y represents a hydrolyzable group, a is an integer of 1 to 3 and
b is an integer of 0 to 2, provided that a+b is an integer of 1 to 3.
[0010] According to a second aspect of the present invention there is provided a thermally
conductive grease compostion (A) 50-95 weight % of an an organosilane represented
by formula, R
IaR
IIbSiY
4-1-b, and/or a partial hydrolysis condensate thereof, and (B) 5 to 50 weight % of at least
one base oil selected from the group consisting of liquid silicones, liquid hydrocarbons
and fluorohydrocarbon oils, wherein R
I represents a 6-20C alkyl group or a group formed by substituting halogen atom or
atoms for part or all of the hydrogen atoms attached to carbon atoms of the 6-20C
alkyl group, R
II represents a 1-20C hydrocarbon group or a group formed by substituting halogen atom
or atoms for part or all of the hydrogen atoms attached to carbon atoms of the 1-20C
hydrocarbon group, Y represents a hydrolyzable group, a is an integer of 1 to 3 and
b is an integer of 0 to 2, provided that a+b is an integer of 1 to 3.
[0011] The organosilane with which an aluminum nitride powder undergoes surface treatment
to function as Component (A) of the present grease composition is represented by formula
R
IaR
IIbSiY
4-a-b. R
I in the formula represents a 6-20C alkyl group, with examples including hexyl, octyl,
decyl, dodecyl, tetradecyl, hexadecyl and octadecyl groups. And the hydrogen atoms
of such alkyl groups may be partly or all replaced by hydrogen atoms. Of these alkyl
groups, 6-14 C alkyl groups are preferred over the others. The number of R
I group(s), which is represented by "a", is 1, 2 or 3, preferably 1.
[0012] R
II in the formula, represents a 1-20C hydrocarbon group, which includes an alkyl group,
a cycloalkyl group, an alkenyl group, an aryl group and an aralkyl group. And the
hydrogen atoms of such groups may be partly or all replaced by hydrogen atoms. Examples
of a hydrocarbon group represented by R
II include alkyl groups, such as methyl, ethyl, propyl, butyl, pentyl, hexyl, octyl,
decyl, dodecyl, tetradecyl, hexadecyl and octadecyl; cycloalkyl groups, such as cyclopentyl
and cyclohexyl; alkenyl groups, such as vinyl and allyl; aryl groups, such as phenyl
and tolyl; aralkyl groups, such as 2-phenylethyl and 2-methyl-2-phenylethyl; and halogenated
hydrocarbon groups, such as 3,3,3-trifluoropropyl, 2-(perfluorobutyl)ethyl, 2-(perfluorooctyl)ethyl
and p-chlorophenyl. Of these groups, methyl group is especially preferred.
[0013] The hydrolyzable group represented by Y is a functional group selected from the class
consisting of a hydroxyl group, 1-6C alkoxy groups, acyloxy groups and alkenyloxy
groups. Examples of such a hydrolyzable group include a methoxy group, an ethoxy group,
a propoxy group, a butoxy group, an acetoxy group and a propenoxy group. Of these
groups, hydroxyl and alkoxy groups are especially preferred over the others.
[0014] Specific examples of an organosilane represented by the foregoing formula include
C
6H
13Si(OCH
3)
3, C
10H
21Si(OCH
3)
3, C
12H
25Si(OCH
3)
3, C
16H
33Si(OCH
3)
3, C
10H
21Si(CH
3)(OCH
3)
2, C
10H
21Si (C
6H
5)(OCH
3)
2, C
6H
13Si(COCH
3)
3, C
10H
21Si(CH
3)(COCH
3)
2, C
6H
13Si (CH
2CH
2C
6H
5)(OH)
2, C
6H
13Si(OH)
3, C
10H
21Si(CH=CH
2)(OCH
3)
2, C
10H
21Si (CH
2CH
2CF
3)(OCH
3)
2, C
4F
9CH
2CH
2Si(OH)
3, (C
4F
9CH
2CH
2)
2Si(OCH
3)
2, C
8F
17Si(OCH
3)
3 and C
8F
17Si(COC
2H
5)
3.
[0015] The suitable amount of an organosilane used is from 0.1 to 30 parts by weight, preferably
from 0.5 to 10 parts by weight, per 100 parts by weight of aluminum nitride powder.
When the amount of an organosilane used is less than 0.1 parts by weight, the aluminum
nitride powder treated therewith is poor in water resistance; while, even when the
amount is increased beyond 30 parts by weight, no increase in treatment effect is
attained, so it means a waste of organosilane.
[0016] When the proportion of the aluminum nitride powder having the organosilane-treated
surface in a grease composition is less than 50 weight %, the resulting composition
is inferior in heat reducing characteristics; while, when it is more than 95 weight
%, the grease obtained is poor in spreadability. Accordingly, the appropriate proportion
of the surface-treated aluminum nitride powder as Component (A) is from 50 to 95 weight
%, preferably from 60 to 80 weight %.
[0017] The aluminum nitride powder used in the present invention is a nitride of Group III-V
metal which generally has a crystal structure of hexagonal system or wurtzite type,
and colored white or grayish white in appearance. The particle shape of the aluminum
nitride powder is amorphous or spherical depending on the preparation method adopted.
[0018] The aluminum nitride powder to undergo the present surface treatment is prepared
using, e.g., a direct nitriding method in which a metallic aluminum powder is allowed
to react directly with nitrogen or ammonia, an alumina reduction method in which a
mixture of alumina and carbon powders is heated in an atmosphere of nitrogen or ammonia
to undergo reduction and nitriding reactions at the same time, a method of reacting
aluminum vapor directly with nitrogen, or the pyrolysis of AlCl
3 · NH
3.
[0019] The aluminum nitride powders prepared according to any of the methods as mentioned
above can be used in the present invention, although they differ in characteristics,
including the chemical composition (impurities), the particle shape and the particle
size distribution, depending on the preparation method adopted. Also, the powders
prepared by different methods may be used as a mixture.
[0020] The thus prepared aluminum nitride powder is a very hard material, and has an excellent
thermal conductivity, electric insulation and mechanical strength.
[0021] Any aluminum nitride powder is usable in the present invention as long as the Mohs'
hardness thereof is in the range of 7 to 9. In particular, aluminum nitride powders
having Mohs' hardness of from 8 to 9 are used to advantage.
[0022] With respect to the average particle size thereof, the aluminum nitride powder having
an average particle size in a wide range of 0.1 to 100 µm is usable in the present
invention. In view of dispersibility in a base oil as Component (B), however, it is
desirable for the aluminum nitride powder to have an average particle size in the
range of 0.5 to 5 µm, preferably 1 to 4 µm, particularly preferably 2 to 4 µm.
[0023] This is because the grease obtained using an aluminum nitride powder having an average
particle size smaller than 0.5 µm is low in consistency (or high hardness and poor
dispensation suitability); while, when the average particle size is larger than 5
µm, the thermally conductive material obtained is poor in uniformity and stability
and, what is worse, the base oil separates therefrom to a considerable extent (namely,
the material obtained has a high oil-separation degree). Therefore, it is a matter
of course that good grease cannot be obtained in the foregoing cases.
[0024] With respect to the specific surface area, the aluminum nitride powders as mentioned
above are usable as long as their specific surface area is in the range of 0.1 to
100 m
2/g. In order to obtain a uniform grease composition, however, it is desirable that
the specific surface area of an aluminum nitride powder used be in the range of 1
to 10 m
2/g, particularly 2 to 5 m
2/g.
[0025] The thermal conductivity of aluminum nitride is 7.7 × 10
-1 cal/cm · sec · °C in theory, but the actually measured value is lower than the theoretical
value, specifically 6.0× 10
-1 cal/cm · sec · °C or below, because the aluminum nitride powder obtained in practice
is more or less contaminated with impurities and contains voids and bubbles. It is
required for the aluminum nitride powder used in the present invention to have a thermal
conductivity of at least 1.5×10
-1 cal/cm · sec · °C at room temperature. In particular, it is desirable that the thermal
conductivity thereof be at least 2.4×10
-1 cal/cm · sec · °C at room temperature. When the thermal conductivity of an aluminum
nitride powder used is below 1.5×10
-1 cal/cm · sec · °C, the thermal conductivity of the grease obtained cannot reach such
a high value as to be aimed at by the present invention.
[0026] Examples of aluminum nitride which can be used in the present invention include US,
UF and UM, trade names, produced by Toyo Aluminum Co., Ltd., XUS-55548, trade name,
produced by Dow Chemical Co., Ltd., H-grade and F-grade, trade names, produced by
K.K. Tokuyama, FA and ES-10, trade names, produced by Nippon Light Metal Co., Ltd.,
and A-100WR, A-100 and AG-SD, trade names, produced by Advanced Refractory Technologies
Inc.
[0027] The surface treatment of an aluminum nitride powder in the present invention can
be effected in a conventional way, e.g., by mixing an aluminum nitride powder and
an organosilane or partial hydrolysis products thereof by means of a mixing machine,
such as TRIMIX, TWINMIX or PLANETARY MIXER (trade names, products of INOUE MFG., INC.),
ULTRA MIXER (trade name, a product of MIZUHO INDUSTRIAL CO., LTD.) or HIVISDISPERMIX
(trade name, a product of TOKUSHU KIKA KOGYO CO., LTD.).
[0028] Therein, the mixing may be carried out while heating those materials up to 50-150°C,
if needed. Further, the mixing may be performed in the presence of a diluent, such
as toluene, xylene, petroleum ether, mineral spirit, isoparaffin, isopropyl alcohol
or ethanol. In this case, it is desirable that the diluent be removed with a vacuum
device or the like at the conclusion of mixing.
[0029] The aluminum nitride powder treated in accordance with the present invention has
great improvement in water resisting properties, and thereby the generation of ammonia
due to the hydrolysis thereof can be inhibited. Thus, the present aluminum nitride
powder not only has high thermal conductivity but also can be used under high humidity,
so that it is well suited to the filler of a heat reducing material.
[0030] Since the present thermally conductive grease composition comprises (A) 50-95 weight
% of the surface-treated aluminum nitride powder and (B) 5-50 weigh % of a base oil,
the diluent used at the mixing time in the foregoing surface treatment can also be
the base oil as Component (B) of the present composition. In this case, the organosilane
or partial hydrolysis products thereof as the treating agent is mixed in advance with
a base oil, and then admixed with an aluminum nitride powder to effect the mixing
and the surface treatment at the same time. The composition prepared in this manner
is also included in the present invention.
[0031] The liquid silicone used as the base oil of Component (B) in the present grease composition
can be properly selected from known silicones which are liquid at room temperature,
such as organopolysiloxanes, polyorganosilalkylenes, polyorganosilanes and copolymers
thereof. From the viewpoint of ensuring heat resistance, stability and electric insulation,
however, it is desirable to use organopolysiloxanes, particularly an organopolysiloxane
represented by compositional formula R
IIIcSiO
(4-c)/2. Each R
III in this formula is a group selected from monovalent saturated or unsaturated, unsubstituted
or substituted, hydrocarbon groups having 1 to 30 carbon atoms, and all R
III groups may be the same or different.
[0032] Examples of such a hydrocarbon group as R
III include alkyl groups (e.g., methyl, ethyl, propyl, butyl, pentyl, hexyl, octyl, decyl,
dodecyl, tetradecyl, hexadecyl and octadecyl), cycloalkyl groups (e.g., cyclopentyl
and cyclohexyl), alkenyl groups (e.g., vinyl and allyl), aryl groups (e.g., phenyl,
and tolyl), groups formed by substituting halogen atom(s), cyano group(s) or/and hydroxyl
group(s) for part or all of the hydrogen atoms attached to carbon atoms present in
the above-recited groups (e.g., chloromethyl, 3,3,3-trifluoropropyl, 2-(perfluorobutyl)ethyl,
2-(perfluorooctyl)ethyl, p-chlorophenyl, cyanopropyl, phenol and hindered phenol),
and functional group-containing hydrocarbon groups (e.g., amino group-containing hydrocarbon
groups, polyether group-containing hydrocarbon groups and epoxy group-containing hydrocarbon
groups). Of these groups, a methyl group, a phenyl and alkyl groups having 6 to 14
carbon atoms are preferred over the others.
[0033] In view of consistency required for the grease composition, it is desirable that
"c" in the above formula be a number of 1.8-2.3, preferably 1.9-2.1. Further, it is
desirable that the viscosity of the foregoing organopolysiloxane be from 50 to 500,000
cs, particularly from 100 to 10,000 cs, at 25°C. When the viscosity is below 50 cs
at 25°C, the grease obtained shows a strong tendency to oil bleeding; while, when
it is above 500,000 cs at 25°C, the grease prepared is poor in spreadability.
[0034] The organopolysiloxane used in the present invention can have any of linear, branched
and cyclic structures. In addition, it is not necessarily a single compound, but it
can be a mixture of two or more different organopolysiloxanes. Although "c" is a number
of from 1.8 to 2.3, it is desirable for the organopolysiloxane to have "c" in the
range of 1.9 to 2.1, because this range enables the organopolysiloxane to have a linear
structure or a structure close thereto.
[0035] Suitable examples of such an organopolysiloxane include dimethylpolysiloxane, diethylpolysiloxane,
methylphenylpolysiloxane, dimethylsiloxane-diphenylsiloxane copolymer, and alkyl-modified
methylpolysiloxanes. Of these polysiloxanes, homopolymers and copolymers produced
from dimethylsiloxane, alkylmethylsiloxane, methylphenylsiloxane or/and diphenylsiloxane
and blocked at their molecular-chain ends with trimethylsilyl or dimethylhydrosilyl
groups are preferred in particular.
[0036] More specifically, such organopolysiloxanes are represented by, e.g., the following
formula (I):

wherein each of R
1 groups is a group selected from monovalent unsubstituted or substituted hydrocarbon
groups having 1 to 30 carbon atoms, such as alkyl groups (e.g., methyl, ethyl, propyl,
butyl, amyl and octyl), alkenyl groups (e.g., vinyl, and allyl), aryl groups (e.g.,
phenyl and tolyl) and groups formed by substituting halogen atom(s), cyano group(s)
or hydroxyl group(s) for part or all of the hydrogen atoms attached to carbon atoms
present in the above-recited groups (e.g., chloromethyl, 3,3,3-trifluoropropyl, cyanopropyl,
phenol and hindered phenol); R
2 and R
3 groups are the same or different, and each of them is the same monovalent hydrocarbon
group as R
1 represents, an amino group-containing organic group, a polyether group-containing
organic group or an epoxy group-containing organic group; R
4 is a hydrogen atom, the same monovalent hydrocarbon group as R
1 represents, the same monovalent organic group as R
2 or R
3 represents, or a hydroxyl group; and ℓ is a positive number to ensure the viscosity
of from 50 to 500,000 cs at 25°C in the organopolysiloxane.
[0037] It is desirable for the organopolysiloxane used in the present invention to be blocked
with trimethylsilyl groups at the molecular-chain ends thereof. As R
1, R
2 and R
3 each, an alkyl group such as methyl or ethyl, an aryl group such as phenyl or tolyl,
or a group formed by substituting hydroxyl group(s) for a part of the hydrogen atoms
of the group as recited above, particularly a methyl group, a phenyl group or an alkyl
group having 6 to 14 carbon atoms, is preferable with respect to easiness of synthesis
and thermal resistance and electric insulation of the oil obtained.
[0038] The organopolysiloxane oil as mentioned above can be produced in accordance with
known methods. For instance, dimethylpolysiloxane oil can be produced by subjecting
a low molecular cyclic siloxane, such as octamethylcyclotetrasiloxane or decamethylcyclopentasiloxane,
to a ring-opening reaction in the presence of an acid catalyst, such as sulfuric acid,
chlorosulfonic acid, nitric acid, phosphoric acid, activated clay, acid clay or trifluoroacetic
acid, or an alkaline catalyst, such as potassium hydroxide, sodium hydroxide, rubidium
hydroxide, cesium hydroxide, potassium oxide, potassium acetate or calcium silanolate,
and then polymerizing the reaction product.
[0039] In order to produce a dimethylpolysiloxane oil having the intended viscosity by controlling
the polymerization degree in the foregoing method, a low molecular weight siloxane
having a terminal blocking group, such as hexamethyldisiloxane, octamethyltrisiloxane
or decamethyltetrasiloxane, can be added properly at the polymerization stage.
[0040] As for the production of organopolysiloxanes having carbon functional groups, on
the other hand, an amino group-containing organopolysiloxane can be produced by the
dealcoholating condensation reaction between an organopolysiloxane having at least
one silanol group and an amino group-containing alkoxysilane, and an epoxy group-
or polyether group-containing organopolysiloxane can be produced by subjecting a compound
having both an epoxy or polyether group and an unsaturated group, such as a vinyl
group, and an organohydrogenpolysiloxane having hydrogen-attached silicon atom(s)
to an addition reaction in the presence of a platinum catalyst.
[0041] From the standpoint of improving, e.g., the thermal resistance, R
1 in formula (I) may be a monovalent substituted hydrocarbon group having the hindered
phenol structure as described in Japanese Tokko Hei 3-131692.
[0042] Examples of a liquid silicone suitable for the present invention include those represented
by the following formula (II)

wherein R
5 is -C
4H
9, -C
6H
13, -C
8H
17, -C
10H
21, -C
12H
25, -C
25H
31 or -C
18H
37; R
6 is -(CH
2)
s-Q; s is an integer of 1 to 6; Q is a group selected from the following monovalent
hydrocarbon groups having hindered phenol structures,

R
7 is a 2-phenylethyl group or a 2-phenylpropyl group; and m, n, p, g and r are each
a number satisfying the following equations: 0≤ m 1,000, 0 ≤ n ≤ 100, 0 ≤ p ≤1,000,
0 ≤ q ≤ 1,000, 0 ≤ r ≤ 2,000 and

.
[0043] However, the organopolysiloxane oils produced in accordance with the foregoing methods
generally contain low molecular weight siloxanes having at most 12 siloxane units
in a proportion of about 10 %, because they are obtained as equilibrated mixtures
of polysiloxanes produced with the progress of polymerization which are various in
their polymerization degrees.
[0044] After the syntheses using the foregoing methods, therefore, the products obtained
generally undergo a stripping treatment at a temperature of 120-250°C under a reduced
pressure to remove the low molecular weight siloxanes therefrom. Even after the stripping
treatment, however, the low molecular weight siloxanes still remain in a quantity
of 500-20,000 ppm. These low molecular weight siloxanes have a strong adsorbing power,
compared with nonpolar combustible gases, so that their vapors are adsorbed strongly
by various electrical contact parts and so on.
[0045] The low molecular weight siloxanes adsorbed to electrical contact parts are converted
into SiO
2· nH
2O by undergoing oxidation, and further accumulated in the form of αSiO
2 on the surface of the contact parts to cause a contact point disturbance. Therefore,
the presence of low molecular weight siloxanes is already known to be undesirable.
[0046] In addition, it is also known that such a problem can be prevented by reducing each
of the contents of low molecular weight siloxanes having no more than 12 siloxane
units to at most 50 ppm.
[0047] The removal of the foregoing low molecular weight siloxanes can be effected by subjecting
an organopolysiloxane oil produced by the foregoing conventional method to a stripping
treatment at a high temperature of 150-300°C under a reduced pressure of 50 mmHg or
below in an atmosphere of dried nitrogen gas, or by extracting the low molecular weight
siloxanes contained in the foregoing organopolysiloxane oil with an alcohol or ketone
solvent. Thus, each of the contents of low molecular weight siloxanes in the organopolysiloxane
oil produced in the foregoing manner can be reduced to less than 50 ppm, and the total
content of the low molecular weight siloxanes having from 2 to 12 siloxane units can
be reduced to less than 500 ppm.
[0048] From the viewpoint of consistency and dispensation property required for a silicone
grease composition, it is desirable that the liquid silicone used in the present invention
have its viscosity in the range of 50 to 500,000 cs, particularly 100 to 100,000 cs,
at 25°C.
[0049] When the liquid silicone as described above is used in a proportion less than 5 weight
%, the resulting composition cannot be in a state of grease and has a poor spreadability;
while, when the proportion thereof is more than 50 weight %, the composition obtained
is insufficient in thermal conductivity. Accordingly, the suitable proportion of the
liquid silicone in the present grease composition is from 5 to 50 weight %, preferably
from 7 to 30 weight %.
[0050] In order to utilize liquid hydrocarbons or fluorinated hydrocarbon oils as the base
oil of Component (B) in the present invention, they are required to have the following
characteristics; namely
1) appropriate viscosity characteristics, including a slight change of viscosity with
temperature and solidification at a low temperature (a low pour point),
2) low volatility at high temperatures and a high flash point,
3) high stability against oxidation and satisfactory thermal stability, more specifically
good receptiveness to the benefit from antioxidants and no changes in color and properties
upon heating up to about 200°C,
4) good oiliness,
5) slight aggravating influences upon surrounding materials, such as sealing materials
and resinous or ceramic cover, and
6) good affinity for fillers (thickeners).
[0051] As examples of a base oil which has the foregoing characteristics and is usable in
the present invention, mention may be made of mineral oils generally used as the base
oil of lubricating oil, particularly the mineral oils of naphthene and paraffin types.
Besides the mineral oils, a wide variety of synthetic oils, setting aside the synthetic
oils of silicone type such as methyl silicone oil and phenyl silicone oil, can be
employed as the base oil of grease having the use under temperatures covering a wide
range, provided that they have more excellent fluidity, viscosity index and thermal
stability than mineral oils.
[0052] Specific examples of those mineral and synthetic oils usable as the base oil in the
present invention include paraffin oil, naphthene oil, α-olefin oligomers (poly-α-olefins),
polybutenes (polyisobutylenes), substituted aromatic compounds, polyalkylene glycols
(polyglycol, polyether, polyalkylene oxides), diesters (dibasic acid esters), polyol
esters (neopentylpolyol esters and hindered esters), phosphoric acid esters (phosphate
esters), fluorinated compounds, such as chlorofluorocarbons, fluoroesters and perfluoroalkyl
ethers (fluoropolyglycols, perfluoropolyethers, polyperfluoroalkylethers), and polyphenylether.
[0053] With respect to the synthetic oils recited above, the α-olefin oligomers include
those represented by the following formula (III), the polybutenes include those represented
by the following formula (IV), the substituted aromatic compounds include those represented
by the following formula (V) and the polyalkylene glycols include those represented
by the following formula (VI):

[0054] In the above formula (VI), R and R'' each are a hydrogen atom or a C
1-20 alkyl group, R' is a hydrogen atom or a methyl group, and n is from 5 to 100. The
compound of formula (VI) is generally polyethylene or polypropylene glycol ether having
H or CH
3 as R and R''. Further, it may be a copolymer of these two glycols.
[0055] The diesters (dibasic acid esters) are generally produced by the esterification reaction
between alcohols and dibasic acids as shown below;

wherein R is H or a C
4-18 alkyl group and R' is a C
4-18 alkylene group or an arylene group.
[0056] The dibasic acids used as starting material are generally those represented by formula,
HOOC(CH
2)
nCOOH, with examples including adipic acid (n=4), azelaic acid (n=7), sebacic acid
(n=8) and dodecane diacid (n=10). The alcohols used in combination with those acids
are 7-13C primary alcohols having a side chain, with examples including 2-ethylhexanol
(C
8), isodecanol (C
10) and tridecanol (C
13).
[0057] By using those acids and alcohols in different combinations, various diesters can
be obtained. Examples thereof include diisodecyl phthalate, di-2-ethylhexyl phthalate,
dibutyl phthalate, diisodecyl adipate, diisononyl adipate, diisobutyl adipate, mixed
acid esters of 2-ethylhexanol, di-2-hexyl sebacate, dibutyl sebacate, di-2-ethylhexyl
azelate, di-n-hexyl azelate, di-2-hexyl dodecanoate and dibutoxyethoxyethyl adipate.
[0058] The polyol esters, including neopentylpolyol esters and hindered esters, are monobasic
fatty acid esters of polyhydric alcohols, such as neopentylpolyols.
[0059] In producing polyol esters, neopentylpolyols which are mass-produced as the starting
material for syntheses of alkyd resin and surfactants can be employed as raw materials
of alcohols. Specifically, neopentyl glycol (NPG), trimethylolpropane (TMP), trimethylolethane
(TME), pentaerithritol (PE) and dipentaerithritol (DPE) can be used as polyhydric
alcohol.
[0060] The monobasic fatty acids usable as the other starting material in the polyol ester
synthesis include straight-chain and branched C
3-13 carboxylic acids. For instance, as C
9 carboxylic acids are exemplified the following acids having a straight-chain structure,
a branched structure and a structure having a neopentyl type branch respectively:

[0061] By variously combining the above-recited compounds as starting materials, a wide
variety of polyol esters can be synthesized. In particular, the esters produced by
the reaction of an acid having a neopentyl type branch with an alcohol having a neopentyl
type branch have the advantage of high thermal stability.
[0062] Additionally, by the comparative experiment on stability against pyrolysis between
di(isooctyl)azelate as an ester produced from an alcohol having no neopentyl type
branch and an acid having no neopentyl type branch, bis(2,2-dimethyloctyl)azelate
as an ester produced from an alcohol having a neopentyl type branch and an acid having
no neopentyl type branch, and bis (2, 2-dimethylpentyl)-2,2,8,8-tetraethylazelate
as an ester produced from an alcohol having a neopentyl type branch and an acid having
neopentyl type branches, it is known that the last ester as the neopentyl type-neopentyl
type combination has the highest thermal stability.
[0063] The phosphoric acid esters include esters prepared from phosphoric acid as an inorganic
acid and phenols or alcohols. With respect to the phenyl phosphate, as triphenyl phosphate
is in a solid state at ordinary temperature, the phenyl phosphates in a liquid state
can be generally prepared by using phenols substituted by alkyl group(s). Examples
of such a liquid phenyl phosphate include tricresyl phosphate (TCP), trixylenyl phosphate,
tripropylphenyl phosphate and tributylphenyl phosphate.
[0064] Suitable examples of an alkyl phosphate include tributyl phosphate (TBP) and tri-2-ethylhexyl
phosphate (TOP).
[0065] The chlorofluorocarbons have a structure such that hydrogen atoms of n-paraffin are
replaced by fluorine atoms and chlorine atoms, and can be produced by polymerizing
chlorotrifluoroethylene in a low polymerization degree as shown in the following reaction
scheme:

[0066] The chlorofluorocarbon produced has a viscosity depending on the polymerization degree,
and the viscosity can be varied over a wide range.
[0067] Examples of a fluoroester usable in the present invention include sebacic acid esters
of C
7 perfluoroalcohols, pyromellitic acid esters of perfluoroalcohols and camphoric acid
esters of perfluoroalcohols.
[0068] The perfluoroalkyl ethers are generally represented by the following formula (VII)
or (VIII):

wherein Rf is CF
3 or C
2F
5, and n is a number of 5-60.

wherein Rf is CF
3 or C
2F
5, and m and n are the same or different, provided that m+n is a number of 5-60.
[0069] It is possible to produce perfluoroalkyl ethers having from low to high viscosities
by changing the polymerization degree.
[0070] From the viewpoints of consistency and dispensation suitability required for thermally
conductive grease, it is desirable that the liquid hydrocarbons and/or fluorinated
hydrocarbon oil used in the present invention have their viscosity in the range of
50 to 500,000 cs, especially 100 to 100,000 cs, at 25°C.
[0071] Further, a thickener can be used as Component (C) in the present thermally conductive
grease composition. As high thermal conductivity is required for the thickener as
Component (C), at least one inorganic powder selected from the group consisting of
zinc oxide, alumina, boron nitride and silicon carbide can be employed as Component
(C). The surface of such an inorganic powder may be made hydrophobic by pretreatment
with an organosilane, organosilazane, organopolysiloxane or organic fluorine-containing
compound, if needed. When these thickeners are used in a proportion higher than 30
weight %, the grease composition obtained is insufficient in spreadability. Therefore,
it is desirable that they be used in a proportion of 0-30 weight %, preferably 0-
15 weight %. It is advantageous to the composition to use a filler having higher thermal
conductivity since it can be used for conferring high thermal conductivity on the
grease composition.
[0072] The zinc oxide usable as Component (C) in the present invention is a white zinc oxide
powder having a hexagonal or wurtzite crystal structure, generally referred to as
"Zinc White". Such a zinc oxide powder can be prepared using known methods. For instance,
one of the known methods is an indirect method in which the zinc vapor generally produced
by heating metallic zinc to 1,000°C is oxidized with hot air, and another thereof
is a direct method wherein the zinc oxide obtained by roasting zinc ore is reduced
by coal or the like and the zinc vapor produced is oxidized with hot air, or wherein
the slag obtained by the leaching of zinc ore with sulfuric acid is admixed with coke
and then heated in an electric furnace, and further the zinc vapor produced thereby
is oxidized with hot air.
[0073] The zinc oxide produced using any of the foregoing methods is cooled by passing through
an air condenser equipped with a blower, and fractionated according to the grain size.
As still another production method of zinc oxide, there is known a wet method in which
a zinc salt solution is admixed with an alkali carbonate solution to precipitate zinc
hydroxycarbonate and the zinc hydroxycarbonate obtained is roasted. The thus obtained
zinc oxide powders are defined in accordance with the Japanese Industrial Standards,
JIS K1410 and K5102, or American standards, ASTM-D79. In the present invention, the
zinc oxide powders produced by any of the aforementioned methods can be used alone,
or a mixture of zinc oxide powders produced by different methods may be used.
[0074] In general the zinc oxide powder is used not only as a vulcanization accelerator
for rubber but also in the fields of coating color, ceramics, enameled ware, glass,
ferrite, cosmetics and medicines. Further, it is known to use a zinc oxide powder
as a thermal conductivity providing filler in a thermally conductive grease [Japanese
Tokkai Sho 51-55870, Sho 54-116055, Sho 55-45770, Sho 56-28264, Sho 61-157587, Hei
2-212556 (U.S. Patent No. 5,221,339), Hei 3-162493 (U.S. Patent No. 5,100,568) and
Hei 4-202496].
[0075] The average grain size of a zinc oxide powder which can be used in the present invention
is in a wide range of 0.2 to 5 µm. In the view of the dispersibility in a base oil
as Component (B) and the relation to the aluminum nitride powder used in combination,
it is desirable to use a zinc oxide powder having a grain size in the range of 0.3
to 4 µm, particularly 0.3 to 3 µm. By using the zinc oxide powder having such a grain
size, the oil separation degree of the thermal conductive material obtained can be
reduced to 0.01 % or below. Further, it is desirable for the zinc oxide used to have
Mohs' hardness of from 4 to 5.
[0076] The alumina powder usable as a thickener capable of providing thermal conductivity
in the present invention is a powder of aluminum oxide represented by chemical formula,
Al
2O
3, and includes aluminum oxide powders generally referred to as Alumina, α-Alumina,
Single crystal corundum fines and Spherical Alumina respectively depending on their
preparation methods.
[0077] In general the so-called Bayer method, wherein bauxite as a raw material is treated
with hot sodium hydroxide, is employed as an industrial manufacturing method of alumina.
In this method, crystals of aluminum hydroxide (Al(OH)
3) are once formed, and then burned at a high temperature, e.g., in a rotary kiln to
be converted into alumina. Alumina has excellent thermal, mechanical and physical-and-chemical
characteristics, so that it is widely used for various refractories, abrasives, porcelain,
white filling pigments, catalysts and so on.
[0078] In general the alumina powder is an α-alumina powder having a crystal structure belonging
to a hexagonal system, and it is a white powder in appearance. Such an α-alumina powder
has an apparent average particle size of the order of 20-80 µm, and each particle
is made up of primary crystalline alumina having a size of about 0.5 µm to about 20
µm. Also, the α-alumina powder can be produced in various grades depending on the
intended use thereof. In the case where an α-alumina powder is used for a silicone
grease, the shape and the size thereof have delicate effects on characteristics of
the resulting grease, including homogeneity and consistency.
[0079] The alumina powder used in the present invention can have its apparent average particle
size in a wide range of 20 to 80 µm, but from the viewpoint of dispersibility in a
liquid silicone it is desirable that the apparent average particle size thereof be
in the range of 30 to 50 µm, particularly 30 to 40 µm. As for the hardness of an alumina
powder, the general alumina is very hard and the Mohs' hardness thereof is from 8
to 9. In the present invention, it is possible to use alumina powders having Mohs'
hardness in such a range.
[0080] The thermal conductivity of alumina is 6.5 × 10
-2 cal/cm · sec ·°C (27.2 W/m°K) in theory, but the measured thermal conductivity of
an alumina powdery product is generally lower than the theoretical value because they
are more or less contaminated with impurities and contain voids or/and bubbles.
[0081] In the present invention, it is desirable to use an alumina powder having a thermal
conductivity of at least 1.2× 10
-2 cal/cm · sec ·°C (5.0 W/m°K) at room temperature. Even if the alumina powder having
a thermal conductivity lower than 1.2×10
-2 cal/cm · sec ·°C is added to grease, it cannot satisfactorily contribute to thermal
conductivity of the grease.
[0082] The boron nitride powders usable as a thickener of Component (C) in the present invention
are boron nitride powders having a hexagonal crystal structure similar to that of
graphite, or a hexagonal network laminate which are produced by heating boric acid
or a borate in combination with a nitrogen-containing organic compound or ammonia.
The boron nitride of hexagonal system has characteristics such that it retains high
lubricity even in a high temperature range, has high thermal conductivity, as well
as high electrical insulating capacity, and further is chemically stable and hardly
wetted with fused metal or glass. Accordingly, it is used as an electrical insulating
filler having high thermal conductivity, a solid lubricant, a filler for modification
of resins, or the like.
[0083] These boron nitride powders having a crystal structure of hexagonal system are white
in appearance, the average grain size thereof is from 1 to 10 µm. Although the boron
nitride powder used in the present invention may have its average grain size in the
foregoing wide range of 1-10 µm, it is preferable that the average size be in the
range of 1-5 µm from the viewpoints of dispersibility in a base oil as Component (B)
and prevention of oil separation.
[0084] In addition, the hexagonal boron nitride powder is generally soft. In the present
invention, the boron nitride powders having Mohs' hardness in the range of 1 to 3
are usable. In particular, the boron nitride powders having Mohs' hardness of the
order of 2 are used to advantage.
[0085] The theoretical thermal conductivity of boron nitride is 60.3 W/m°K at room temperature,
but the measured thermal conductivity of a boron nitride powdery product is generally
lower than the theoretical value because the product is more or less contaminated
with impurities and contains voids or/and bubbles. In the present invention, it is
desirable to use a boron nitride powder having a thermal conductivity of at least
5.0 W/m°K at room temperature. Even if the boron nitride powder having a thermal conductivity
lower than 5.0 W/m°K is contained in grease, it cannot satisfactorily contribute to
thermal conductivity of the grease.
[0086] On the other hand, the hexagonal boron nitride as described above is converted to
cubic boron nitride based on the same structural principle of diamond when it undergoes
a high temperature-ultrahigh pressure processing. The boron nitride having a crystal
structure of cubic system has the hardness second to that of diamond, and its powdered
products available on the market are from liver brown to black in appearance and the
average particle size thereof is in the range of several µm to 800 µm.
[0087] Such cubic boron nitride powders also are usable in the present invention, but they
are not favorable because their thermal conductivity is in a low range of 0.5 to 3.6
W/m °K; as a result, even if they are added to grease, the achievement of high thermal
conductivity aimed at by the present invention is difficult.
[0088] The silicon carbide powder usable as Component (C) in the present invention is generally
obtained by producing high-purity α-SiC ingot from silica and coke as the main raw
materials by means of an electric resistance furnace (Acheson furnace) and subjecting
the thus produced ingot to pulverizing, decarburizing, iron-removing and sieving steps
in succession. This process can provide silicon carbide powders having various particle
size distributions depending on the intended uses. Further, an ultra fine silicon
carbide powder can be prepared by choosing a powder having a moderate particle size
distribution as starting material, thoroughly grinding the powder into fine particles
of sub-micron order in size, sieving them, and further purifying by a chemical treatment.
[0089] The particle diameter and the particle size distribution of silicon carbide are determined
by the methods defined in JIS R6001, JIS R6002 and JIS R6124. The average particle
size of a silicon carbide powder used in the present invention, though it may be in
the wide range of 0.4 to 10 µm, is desirably in the range of 0.4 to 5 µm from the
viewpoints of securing high dispersibility in liquid silicone and preventing oil separation.
The silicon carbide powders are bluish black in appearance, have a crystal structure
of trigonal prism, and are generally hard. With respect to the hardness, silicon carbide
powders are usable in the present invention so long as they have Moh's hardness in
the range of 8 to 9.
[0090] The theoretical thermal conductivity of silicon carbide is 2.4 ×10
-1 cal/cm·sec·°C (100.4 W/m°C) at room temperature, but the actually measured value
is lower than the theoretical value because the silicon carbide powder obtained in
practice is more or less contaminated with impurities and contains voids and bubbles.
It is desirable for the silicon carbide powder used in the present invention to have
a thermal conductivity of at least 1.2×10
-2 cal/cm·sec·°C (5.0 w/m°K) at room temperature. Even if the silicon carbide powder
having a thermal conductivity lower than 1.2×10
-2 cal/cm · sec ·°C is added to grease, it cannot confer satisfactory thermal conductivity
on the grease.
[0091] In preparing a thermal conductive silicone composition according to the present invention,
at least Components (A) and (B) of the aforementioned Components are mixed with a
mixing machine, e.g., TRIMIX, TWINMIX or PLANETARY MIXER (which are the trade names
of mixers made by INOUE MFG., INC.), ULTRA MIXER (which is the trade name of a mixer
made by MIZUHO INDUSTRIAL CO., LTD.) or HIVISDISPERMIX (which is the trade name of
a mixer made by TOKUSHU KIKA KOGYO CO., LTD.). The mixing may be carried out under
heating at 50-150°C, if needed. In order to make the thus prepared mixture homogeneous,
it is desirable that the mixture be subjected to a kneading operation under high shearing
stress. Examples of a kneader usable for this operation include a three-rod roll kneader,
a colloid mill and a sand grinder. Of these kneaders, a three-rod roll kneader is
used to advantage.
[0092] The present grease compositions thus prepared have considerable improvement in water
resisting properties, and can steadily retain hardness (consistency) and thermal conductivity
over a long period.
[0093] The present invention will now be illustrated in more detail by reference to the
following examples.
[0094] The entire disclosure of all applications, patents and publications, cited above
and below, and of corresponding Japanese applications No. Hei 10-230587, filed August
17, 1998, and No. Hei 10-232074, filed August 18, 1998, is hereby incorporated by
reference.
PREPARATION EXAMPLES OF SURFACE-TREATED ALUMINUM NITRIDE POWDER
Moisture-proof Test:
[0095] The moisture-proof effect of the present surface treatment on an aluminum nitride
powder was evaluated as follows; After placing 5 g of an aluminum nitride powder and
95 g of water in a 250 ml plastic container with a stopper and putting the stopper
in the container, the container is shaken for 24 hours at room temperature by means
of a shaking machine. Then, the contents are filtered through a filter paper, and
the pH of the filtrate is measured with a pH meter (Model F-15, made by Horiba Seisakusho
Co., Ltd.). The moisture-proof effect is evaluated by the thus measured pH value.
Preparation Example 1:
[0096] In a 5-liter PLANETARY MIXER (trade name, a mixer made by INOUE MFG., INC.), 10 g
of an organosilane of formula C
10H
21Si(OCH
3)
3 and 1,000 g of an aluminum nitride powder (amorphous, average particle Size: 2.0
µm, specific surface area: 4.0 m
2/g) were placed and mixed with stirring for 30 minutes at room temperature. The thus
surface-treated aluminum nitride powder is referred to as Component (A-1) hereinafter.
This powder was subjected to the aforementioned moisture-proof test, and the measured
value of pH was 7.0.
Preparation Examples 2 to 4:
[0097] Surface-treated aluminum nitride powders were prepared in the same manner as in Preparation
Example 1, except that the organosilane of formula C
10H
21Si(OCH
3)
3 was used in different amounts, respectively, as set forth in Table 1. These powders
are referred to as Component (A-2), Component (A-3) and Component (A-4) respectively.
They were also subjected to the aforementioned moisture-proof test, and results thereof
are shown in Table 1.
Preparation Examples 5 to 8:
[0098] Surface-treated aluminum powders referred to as Components (A-5) to (A-8) respectively
were prepared in the same manner as in Preparation Example 1, except that the organosilane
of formula C
10H
21Si(OCH
3)
3 was replaced by organosilanes of formulae C
12H
25Si(OCH
3)
3, C
6H
13Si(OCH
3)
3, C
10H
21Si(CH
3)(OCH
3)
2 and CH
3Si(OCH
3)
3, respectively. They were also subjected to the aforementioned moisture-proof test,
and results thereof are shown in Table 1.
Table 1
Ingredient |
Amounts of Ingredients used (g) |
Aluminum nitride powder |
1000 |
1000 |
1000 |
1000 |
1000 |
1000 |
1000 |
1000 |
C10H21Si(OCH3)3 |
10 |
5 |
50 |
100 |
0 |
0 |
0 |
0 |
C12H25Si(OCH3)3 |
0 |
0 |
0 |
0 |
10 |
0 |
0 |
0 |
C6H13Si(OCH3)3 |
0 |
0 |
0 |
0 |
0 |
10 |
0 |
0 |
C10H21Si(CH3)(OCH3)2 |
0 |
0 |
0 |
0 |
0 |
0 |
10 |
0 |
CH3Si(OCH3)3 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
10 |
Treated aluminum nitride powder |
A-1 |
A-2 |
A-3 |
A-4 |
A-5 |
A-6 |
A-7 |
A-8 |
pH |
7.0 |
8.2 |
6.9 |
6.8 |
7.0 |
8.0 |
7.3 |
10.3 |
EXAMPLES 1 TO 11 AND COMPARATIVE EXAMPLES 1 TO 4
[0099] Thermally conductive grease composition samples were each prepared as follows: Three
Components A, B and C as set forth in Tables 2 and 3 were weighed out in their respective
amounts (parts by weight) as set forth in Tables 2 and 3, placed in a 5-liter PLANETARY
MIXER (trade name, a mixer made by INOUE MFG., INC.), thoroughly mixed for 30 minutes
at room temperature, and further subjected to a kneading process for three times by
means of a three-rod roll.
[0100] The grease composition samples thus prepared were each examined for moisture-proof.
Specifically, the moisture-proof evaluation was made by placing each sample in a thermo-hydrostat
regulated at 40°C-95% RH and measuring the consistency and thermal conductivity of
each sample after 1-day storage, 7-day storage and 1-month storage respectively. Since
the surface-treated aluminum nitride powder undergoes no ageing as long as it retains
its moisture-proof, change in consistency and thermal conductivity of a grease composition
was employed herein as a criterion for evaluating the deterioration in moisture-proof.
[0101] The consistency of each grease composition sample was measured in accordance with
JIS-K-2220 and the thermal conductivity thereof was measured with a hot-wire instrument
for measuring thermal conductivity, Model TCW-1000, made by Shinku Riko Co., Ltd.
The results obtained are also shown in Tables 2 and 3.
[0102] Additionally, the symbols B-1, B-2, C-1 and C-2 used in Tables 2 and 3 stand for
the following materials, respectively:
B-1

viscosity: 390 cs at 25°C B-2

viscosity: 500 cs at 25°C
C-1
Amorphous zinc oxide powder (average grain size: 0.2-5 µm)
C-2
Amorphous alumina powder (average grain size: 30-50 µm).
Table 3
|
Component |
Comparative Example |
|
|
1 |
2 |
3 |
4 |
Amount mixed (g) |
Component (A) |
A-1 |
450 |
980 |
0 |
0 |
A-8 |
0 |
0 |
800 |
0 |
Untreated AlN powder |
0 |
0 |
0 |
800 |
Component (B) |
B-1 |
500 |
20 |
200 |
200 |
B-2 |
0 |
0 |
0 |
0 |
Component (C) |
C-1 |
50 |
0 |
0 |
0 |
C-2 |
0 |
0 |
0 |
0 |
Consistency |
After 1-day storage |
400 |
non-grease |
290 |
288 |
After 7-day storage |
390 |
245 |
solidified |
After 1-month storage |
390 |
solidified |
solidified |
Thermal conductivity (W/m°K) |
After 1-day storage |
0.9 |
2.7 |
2.7 |
After 7-day storage |
0.8 |
2.1 |
- |
After 1-month storage |
0.8 |
- |
- |